Method of treating copper-bearing substances.



criaizilns' suntan my, or NEW Yomr, iii; ASSIGNOR 'ro nnannni oorrnn. rnoo'lsss Be. itknownathat I, CHARLE S. BRADLEY, f'a I'citizen -'0 the United States, and; a'- resideritioflthe rough of Manhattan; ,city,

a ncauhiaaa Juli 23 I me'ntsinMethods of- Trea'ting 'CopperwBear- *ing Substanees,'o'which the following is a speeificatiomj 9-: invention -r e lats -sto :-the chemical treatmentf copper; bearing substances to ooncentrate their values-and is particularly- 1 Many copper bearingores;- contain mixed adaptedto the treatment of low" grade 011-.

I v a copper compoundsg 'such as oxids,carlionates, fsulfid'spand the-like and: metallic =copper.x-

' {In mosti'cases,-and particularly in low'gra'de ore, the values area'ssociated "with relatively;

,hoteconomically;he -treated directly for the ,l-iecovery by".inechanicalconcentration ex- 1slo'st2' "r0 'obta'ina-more perfect concen-' tratign and avoid ,so far as possible this enemas: waste of values 5 numerous at- -tmptsat wet or 'chemical methods of'con- ;.rego,very= of;metal4 3 7 order to eliminate,- fso; .far sasmractmable, the gangue, v'arlous -content: InAfa'ctin very. fewcases does the fcen tiation have been made, .but' these, for

cpimnerqial success so thattheinechanical .iiiletlipd of concentration is p ractiieally the "'oiilf are; found in 'co'mmerci'al' use today;

4 -'va'ri'ousreasqns, have met w'ithlittle oino Some fores, moreoxfer', although containing 'i "clipper and other; values. whieli'git would be *profitable,to'=concentrate orejx' tract' are-not adapted 'to mechanical "value dbj'cl'ib a m-sat sfies bifide comramr o1; mass crgry nnw anasnsr, a coaronuron or ratenteulbee-i'z "1911. J l a. a

I It -.g concentration, and; at less; 99st,", and also I to concentrate or recover othe values from those ,or"other methods in practical ns e; g It 1 s .wellknown that-each of thepvalues contained n the ore cant; be. brought into bring =them'al1 ii -at one 'operationzgln ,ma'ny =cases, furthermore, eonsiderablmdifiiicultyg is ,i-met. with. infiltering, settling; or

:;- My invention provides an; economical chemical method oi concentrating theValues, and comprises broadly the; use of a chlorin which lwaste products I are made xinsoluble and-,.the.-values taken into solutionandliremoved from the gangue and non metallic 'constituentsfof the ore or other -material;

treated} and from-which.=solution the; values may afterward'be recoveredliszi The concentratiom ors extract on off'the {values aschlorids presents emany advantages,- a1n0ng= which in ay be mentfionedft'hfl, rapidity and completeness of so1ution,"=-and the facility of filtratioh; separation ifnom Um ED S E mmomca ..Qres ,wh1 m t r, hareotlf reanq suited; or, profitahleto treat bymechanica'l solution (by some chemical agent but there are few,if any,'-chemical agents whichwill otherwise separating -the,.-soluti on {from the. A gangue and suspended particlesandg'flso recovering the values? irom' the carrier.

compound as acarrier and .transformery'bj theslimes-and gangue.an d=precip.itation or recovery of the metal; But the I provision of asuitable chlorin carrier presents anumberof problems which I--have succeeded in solving by the present invention. Lem-ploy --=for this purposea chlorin -carrier -which will yield up its chlorin to thevalues to and at? the same-time -form insoluble cjom: pounds with the substances with which the values are combined, such asit'he" sulfur or eium chlorid possesses the dcsi'redand other" favorable requisites as a chlorin 'carr'ier, among the latter being that 1t is -inexpensive, and-readily and 'easib' obtained .or manu-l 'fa'ctur'edin theVi'cimt-y 0f the work and that it i's'ea'sily 're'vi'vifi'ed or regenerated for I continuoususein' thepro'c'ess.

In ordenthatthe 'chlorin compound shall jbecome effective in dissol ing the 'values,

"the presenceof an" acid, radical is required.

form soluble chlorid compounds therewith,- I

acid constituents. I have'found th'afi'cal- Thisimay be secured by the direct addition-' of a suitable acid or. its salt,s u'ch for instwl'ice as sulfuric acid; whichnotonly rehde-rs the fchlorin, coinpound effective to dis viz. calcium and 'sulfuricacid,' in the form -'-possiblethematerials found associated with. the copper ores as the'places where these the necessary acid radical, and any GXCgsS withvthe iron oxids or hydro-oxids or solu-j L to bring in a. small quantity of calcium the wastes as the chlorin is retained-in sowhenthe values areprecipitatcd, as will Probably the simplest emhodii'uent 'ofthis carbonates Considering the copper sulfateof-copper and iron,- -and theoretically for the solution-of each-2% of copper we re-? pen. IMy invention therefore aims to effect acidification Iof the copper compounds, and also ,for :absorption to prevent 'contaminat- 'eration employed according to my invenfrom solids is accomplished with great ra with caleiuin chl'orid this salt forms directly 0 content isih soluble form whereas the cal- -66. c'ium sulfate which does not contain any solve the -values but also forms an insoluble precipitate of the intermediarysubstances,

of calcium==snlfate.-- instead, however, of directly adding'the acid it is prefeiahlefor economy-to use for thispurpose as far as ores ;,are=f ound are generally rehiote from sources of chemical supplies Most copper ores contain considerable sulfur ras. sulfids -ble silica" produces compounds which -seriously interfere with the separation of the gangue from the solutions either by settling o'rf filtering; I have found, however, that by replacing the sulfur compounds-by chlorin compounds, under s the conditions of option, filtration or other separation of liquids pidit-y and completeness.

To operate my process it is only-necessary chlorid to initiate the process and make up lution, and the calcium chlorid regenerated.

shown further on. .-,()he of the principles employed in. ac cordance' with myinvention is to convert the values -into copper chlorid which issoluble in calcium chlo'rid solution and to pre-1 cipitate the-values (in the form of copper o xid) by the addition of calcium carl'ionat'c.

principle is found in the formation'of cupric e'hlo'rid. from copper sulfate which is produced 1n.-"a prelim nary amphidlzing or roasting-s ep, and the. sequent prec pient by earcu m .tation ()fli the-1"" alone it ',wi11;be=.- hserve d-hat in contact cupric ehlorid and "calcium sulfate CuSO; -}-Ca'("ll. =C uCl +QaSO Here it will be observed that the'copper values is v insoluble, and hence precipitates. In other words, the calcium chlorid solutiontaks. up only thew-allies as distinguished forexarnple from a 's'odiumchlorid solution which in the reaction referred to would produce sodium sulfate which, being soluble, would remain inthecarrier. The compli-o cations arising from the presence of sub-' stances other than thevalu'es inthecarrier are thus to this extentfelim'inated, The calcium chlorid has another important advantage in the subsequent operations; The solution loses calc um ujhlclrgoes into the formation of the calcium ;sulifate as aboveindicated. The'chl'(n'i1'1,' however, is con served in the copperchlorid. The regeneration 'of the carrier 'a nd the precipitation of the values in a highly concentrated form may thus be accomplished in asimple-andrapid reaction byintroducing calc um car- 35 bonate which is a plentiful and hence inexpensive substance. ()mitting the water of hydration for the sake -o"f simplicity here asoelsewhere, 'the' reaction in this instance the calcium carbonate as follows:

the temperature is highenough todriveofi' the CO and as thissuhs'tance has a copper icontenpof about 80% the flhigli degree of \concentration willhe apparent; It will also jbc' seen that'calciuin chlorid is regenerated. 1

"Aside from the more apparent advantages which the'u'se of calcium chlorifd has been shown to mssess, it is found thatfthe difficulty which is usually met i'ith infilte'ring;

settling or otherwise separating um solids' no to clogging'is largely done away with as by' maintaining the calcium chlorid in the liquid the clogging is preventedand'the firom' the liquids irroperations of this kind moth facilitated.

ll m at-i118 understanding of the general prmelp es mvolved m-my invent on, it Will.

now be seen that-the method provides for the conversion of practically all of-the cop- 'per values contained in the ore into copper 'chlorids. For an un lcrstamhngof the various reactions a more complete description of the details is necessary:

=In the preferred'form of my invention the 120 first step is to subject the crushed and finely ground ore to a prelimiary'amphidizing by which is incantgi'nthis instance, the direct 'forming of a sulfate by the absorption of .oxygenby a sulfid.' 'This-step'involyes heating the crushedoreto a temperature of from 450 to 550 (Lgwith access of air, by which oztidation occurs. Of course-the specific" re actions wh ch take placewlll Vary with the character of the ore, and the inanagementof.

talte'splace between"thecu'pric'chloridsand 90 Here it will be 's'e en that the alues are in the form of copp'cr 'oa id, assuming that 95 How f; the-liquid through-theseparating 110 to sulfate as described and most of. the iron usually present in the ores is converted into ferric oxid, which bein insoluble does not go into the solution ut. remains in the gangue. In practice, however, some of-the 11011 is converted .to and remains as ferric sulfate, a small ortion of the copper remains as the sul d, another small portion Dust and fumes containing sulfurous and sulfuric anhydrids, are also produced. .These compounds and the dust and fumes serve a useful purpose in the process, as will beshow'n,

, so that the-amphidizingor-roasting treatment need not be always complete, and variations in the 'operation of this apparatus will not afiect-finalresults. This isja as,

ture of greatadvantage as it relieves the amphidi z'mg apparatus from the necessity of a strict and constant supervisionfiTh'e mass of amphidized orroasted ore is brought into association with an excess of the calciuin chlorid solution preferably at a little .below boiling temperature in a reaction drum. As above explained cupric chlorid is produced bythe reaction between thec'opper. sulfate and calcium chlorid. The ferric I "sulfate remaining in the mass coining from the amphidizer reacts with the calcium 1 T chlorid to produce ferric chlorid which dissolves and calcium sulfate which is insoluble. "This ferric. chlorid performs the useful function of dissolving the co per ox'id remnant v as well as the copper o the copper 'sulfid the same into copper, chlorid flIf the ferric chlorid is insuflicient in quantity to dissolve all these remnants the balance 'is dissolved by the cupric chlorid, or "the free acid formed i by the action of the calcium chlorid on the amphidized ore as will be more fully pointed I I out below.

Owing to the completeness of the reaction 'Ylin the amphidi'zer, a comparatively small :amount of sulfur remains 'mgaseous form. *Thisjgoes out in the'fo'rmof sulfurous and sulfuric anhydrids in proportions varying,

in Instances so far tested, from 24 to 3-1 The reaction with the S0, is morefully de-, scribed hereafter in connection with the full description of the process. i v

in the with the calcium chlorid which may react with any cupric oxid present to form directly further quantities of copper chlorids:

' The cupric chlorid is soluble fwith the calchlorids into chlorids is .necessary.

ate the solution,

I I i V V clum chlorid, whereas the calcium sulfate precipitates as before. duced from these various sources has an i'm- The cupric chlori d' proportant function aside fromits being'solufid remnants 'notta kencare of by the ferric chlorid as above referred to. With these substances it-produces cuprous chlorid.

becomes oxidized to 'copperoxid and 1n some I cases the ore may contain metallic copper i i which may escape oxidation.

The sulfur in the last reaction'precipitates i so that here again it will be seen that the waste product s not taken up by the'carrier.

It is necessary that suflicient cupric chlorid shall be present to insure that there Wlll not and preferably itshould b61111 excess, To this end the ,cuprous chloridis converted to the cupric condition by; supplying air at a suitable part or partsof the apparatus so be any remnant of copper values lllldlSSQlVda that the cuprous"'chloridsv are oxidized, as o acid with the calcium'chlorid is converted' into cupric chlorid which is taken up by the carrier,'the by-productbeing water. a 1

of the hydrochloric acid Cu O+2HCl=Cu,Gl +H 0.

talies'place'as above indicated;

The presence of insoluble oxychlorlds of copper and iron in the; solutions, woulcl tend to clog the oxidizer'towers 1f per-.

mitied to'remain, and therefore the'presence of anacid radical in sufficie nt' quan- Any cuprous oxid remnant in the reac-- tlon drum forms cuprous chlorid with some I p Q The oxidation of this and "Medan and metallic copper remnants, convert1ng quantities of hydrO-ChLOmQH-ZIl-Qd titv in'the solutions to convertall'the oxy The copper chlorid is "further:

tained in pthe cup ric state by the action theiron chlo rids formed from ferric remnants in the reaction drumIfl These liron chlorids ac'tin onjthe cuprous cl lojrids con vert them to t e cu r1c state and so regenerquantities of gold silver present in, the ore which can be brought into solution by making all the. copper into cupric chlorid and all; the soluble ironinto ferric salts, and

then adding a small amount of ch1orin,

chlorous" or chlo ric compounds. The chlo cium chlorid solutions, may vbe ith-the copper or separately t From the foregoi ng descriptidn pf {the formation of the solutionsitlwill "befseenhere will also be small that calcium chlorid'. acts as an initial or primary dissolving medium, taking into solution certain of the values, and these values practically tion which might are converted by the calcium chlorid into a chlorid, as the cuprous compounds are not.

precipitated by the calcium carbonate. ;The fact that the solution formed is itself an active solvent of the. values is a feature, of

great advantage since the excess solvent power insures completeextractioneven the attendant does not pay 'close attention to the conditions of operation. Accordingly as already noted in connection with the amphidiz'ing" step,- the 'jsolutionapparatus likewise does not require the strict attenand the success of the process is not dependent upon the degree of care exercised by those in charge of the operationsfthus not only gaining the'desired completeness .of'extraction but at the same time accomplishing this with low labor cost. taken all the values into solution rids in the manner above indicated, the

Having mass of gangue solutions and precipitates is then subjected to filtration wherebythe solid matter is eliminated and a clear solution comprising a carrier and the values is in condition obtained.- Preferably the solution'is subjected to a further oxidation in order to insure that the values will all be combined attheir highest valency. The solution is then the solution may contain iron and aluini-" num compounds in addition to those of cop.- per. 'Any arsenic which may have been present in the substances treated will' have been separated by the filtration as arsenic is rendered insoluble. In orderto separate the copper content from the solution I prefer to employ calcium carbonate 'inasmuch as this produces 'a precipitate of cupric oxid and .at the same. time regenerates calcium chlorid. The carbon dioxid evolved by reaction keeps the mass, in

slight agitation, thusassisting in the; access of the precipitating medium tothe substance to be precipitated. Inasmuch as cupric oxid will react with iron and aluminum compounds as soon'as it is formed, the iron and aluminum preclpitation must be otherwise be necessary as chlofont-treatment for the separa tion of values therefrom.- In this condition completed before any precipitate of cupric oxid can remainand be recovered. On the other hand, the presence of the iron and aluminum salts, especially the iron, in the solutionis desired as they are useful in the absorption of fumes and as already pointed out also play an important part in taking the values into the solution. thesecorisidcrations I divide the solution containing the values and subject a portion of itgto precipitation, the other portlon being diverted and utilized in the consumption of fumes asj will hereinafter appear. The proportion of the solution which is to be subjected to precipitation forrecove r'y of the values may be determined by theincrement of values taken'into solution at each cycle or it'may be governed by other circumstances within the discretion of the opera tor. By thus subjecting only a portion of .the-entire quantity of solutions cipitation the 'necessity the iron andaluminum compounds before the incrementof copper values can be ob tainedas cupric oxid and the necessity of filtering this increment fromthe entire mass of'solutions are avoided; while at the same of precipitating all In view of to .prc-

time the increments of lron and aluminum aa-e precipitated and a sufiicient quantity of iron compound retained for the absorption of fumes and taking of values into solution.-- 1 The precipitation of iron and aluminum compounds may take place separately or at the-same time with the precipitation of the copper content. I may employ 'cupric oxid orhydrate or calcium carbonate as the preliminary precipitating medium for the iron and-alununum. Any small quantities of pepper which may be carried down with the 1ron and aluminum may be recovered by returning the precipitate of iron and aluminum-to the amphldizer as the effect of the amphidizer is largely to render the iron and aluminum insoluble whileleaving'the copper in soluble state.

Having rid-of iron and.

aluminum the portion of the solution'subjected to precipitation, the copper content may then be precipitated as copper oxid (usually carrying a little chlorin, as set forth and claimed more specifically in another application to be filed by me) by the addition of calcium carbonate thus regeneratirg the calcium chlorid as already indicat CuCl +CaCO '=CuO+CaCl +Co The precipitate may then be filtered from the remalnlng solution and subjected to such furtiier treatment as may be desired for the production of metallic copper or, any other desired product thereof.

No matter which of the various methods of precipitation above described may be used it is necessary that the iron and copper salts quite; complicated, .the iron may exist as' a] bivalent salt or a 'ti'ivalenh'theeopper may I ,,;exist asa-Jmivalenton bivalent, If an m,

tionsare our h t .ple 'supply of. oxygen orf'chlorin be, present gtghe imp'pergx vill lie inl thejbitalnt condition chlofin vt-h'e that'the:;cu15i io ehldrid-remainsiin'isolutioii} The euprous: chlorid being muchle ss soluble n :woul d he precipitated -11 th an ithe .ouproiis' ohlorid';' therefore in case of; depletionlwefhave largely t-fe oils chlorid}- "and cujirio; :hlorid in ,,solution,;- 1 It might here be. mentionedtl1'at: the: feri ous; chlorid' isa verysolublesalt so. that esga rwhole the:

i iron and popper 'chlorids when together, 1'8: v. :mam ma IIlOI'GSQlllblGCOHdltlQIlJilIl. case of.

reduction. than eo'pper alone.

hlorids, would I 7: .K V on preeipitationby carbonateof celoium & new conditionis.introduoed, :isthe'gron would be precipitated from' the ferrous chloridas ,fierric oxid while. {the "copper.

chlorid is; reduced ;'to euprou schloridvand:

vta'rbonate' of calcium "drofiidffroniicuririeuchlorid. This demonstrales the-neceseity-of having the salts-in the-highesti 's'ta'te f'oxida-tion or chloridetion for the-p er and economical preoipi-l tation. f I find that from the lowsolubility ofothe cuprouschlorid, when it is-allowed to exist,

in the solutions, on precipitation with calhaving li'eeri.'taken' up by the lime'of the Calcium earb'onate) it absorb sioxvgen *from' the air wherever exposed, forming oxychlorid of copper which is insolnblethusclogging pipes, filters, etc; --For' practical operation the necessity for maintaining these salts in compounds of their highest vvalency is evident.

Ther re:

in, case ofQdepletionf the. "solution Pas chlorid ofzin'o {and eoouinu- ,ilzites. fThisfihettl is not precig'iteted (hiring theipreipit'ationiof nb ammnum an'd-oopperj above described, end while its presence 3;; rhe fsolution s fisf nounsien .in' small quantitiesjitiahaX. nevertheless accumulate to 'suqh an "extent as' td make it necexiairy" to eliminate it. I For this purpose the-solution ora'partjoi it which has had the aluminum and iron andieopper removed from it, may

be subsequently -'tr'eate'd,='v vhendesiiie'd, with burnt lime for the precipitation'ofthe zinc. Ahy gold'and silver-v present in the solutions maybe carried down 'during the precipitai n t e i lum iu end v we a subsequently removed or. separated there-.,

-from-, 1n any.,preferred ,1 manner known to those skilled i'nthis artl A'fter filtration, the

solutions which have given up the values iand'taken-in the regenerated-calcium chlorid' e eth me.ieq die e-L q k n h r f'quantities of values into s'oluti'on,--and may be t tume to go. gh i gey e" 9i i p' ,erations which has been '(les'rlribed;-

I fReferring again to the, initial. am' hidiz V f ing'step it should be stated-that oonsi 'rable dust andfume'sKeither or-both of'which are" '.here inafter referred toas the volatile products 'of tlie amphidizer) are given off and these. contain rsulfurous and sulfuric anhy-j. i drid; Iv have' found it difiicult to-approach wat'en hoilin g. temperatures in the drums when any considerable body of gas or air is introduced, intoth'ern on account of the partial pressures:

. into the drums containing the .solution evaporation takes place so rapidly that it is difv 'ficult to raise the temperaturesto anything Y; iwh enzthevolatile produot s are introduced like-a Wa-temboiling heat andasthe reac'-' tion drum should-be as nearyboiling textiperature. as possible, I prefer to take the dust 'and fumes into a separatedrum, where they can be collected at relativelylow tem peratures-in the. diverted portionjof the so-' iutionsj ill containingjhel high valency compounds. The solutions. may then-be taken to the reaction drum where they-can" be maintained: at higher temperature than, 'would be possible if {current of gases or volatile produpts were a1lov'ved-topass ther'ethrough." The sulfuric v ai nhydrid inth'e ires ence ofwater o'ontained in e the solutions unites with-one'of the acid exchanging salts 'sue'ha's calciuin chlorid or iron chloridforrninghj drochloric :a'cid and-thesulfate of the" acid exchanging "salt. iThesulfurous .an-

hydridt'in'the-presefice-of water'unite with the cupric. chlorid "or any'r'emaining ferricchlorid retained in the solution, form- -ing' sulfuric acid, cuprous chlorid, ferrous chlorid and-hydrochloric acid. The columns chlorid, ferrous chlorid and hydrochloric;

acid thus formed will, upon'oxidation, -pro duc'e cupric cbloi-id, ferric chlorid and water,

and the sulfuric acid in the presence of 'cal-- cium chloridwill be converted into sulfate of calcium and hydrochloric acid. The dust and fumes referred to mayor may not contain sufiicien't oxygen to complete the-oxidm tion'ofthe substances of- Variable valency and hence the material coming from the dust and fumes absorbing apparz'itus is preferably subjected to further oxidation to insure that any deficiencywilL-be made up. The mass may' then be introducedinto the solution- 'th solutionsgenerally contain no free acid -titi'es of core or other copper. bearing sub-. stances in .the shortest possible time'and. with" the greatesteconomy, the ntethod should be carried on in a continuous man-.

and this may be explained by the absorption of'the acid byany ferric hydrate or alu1ni-.

nur'n hydrate formed from-the reactions and especially from the oxidation of the ferrous that method and apparatus is to returna'g port ionof the dry slinies in a cyclic manner and inix them with plastic slini'cs', 'so that a 90 chlorid. a a -In:order to 'be able to treat large quanner. .-\n,ap )arat.us suitable-for.this purpose is indicated-1n the auzcompanying'drawing;- It will be uoted..from the description ft-hercof that by this apparatus the copper -.beari'ng substance 'is continuously received 01' taken into the. 'ap'paratus and subjected inn-continuous and cychemanncr to the Van ous-steps'of the process. Stationary tanks and -decanti1 1; tanks are particularly avoided as necessarily -,interm.ittcnt. in operation and limited in: capacity, and incapable of, cconomicalseparation of gangue from liquids carrying the yalues; 'lhe capaeityot the .minor partwis .such that any tc nporar interruption'iu the operation of oneof these .elemcntsdocsnoti disturb the continuity of operations; inasmuch as the other steps may s'tilicontinuc. The filtering:- step involves Incl-said tof'be continuous. Of'co tit-e a vplurality'of filters are use;

the f lt ring continuous v thmformation of cake which must be re moved either continum sly or at. intervals; but whether thisv removal ofthe eake' from" the filters be continuous or intermittent the. process asawhole nc'vc 'tlieless continu-.

ous, inasmuch as the capacity of the ap 'paratus peru'iits theot her operations 'tocontinue during theinterval of time required don -i1 termittently and .a

J]. ein pr cake remoyed trh'mlthem successively.

I In the drawing the gene 'al arrangement" of apparatus suitable for the treatment of indicated in diagram.

ore or other copper bearing substance .is

lindicates r. hcpper communicating with a drier cylinder. 2 and supplied with heat fromsuitable 'meanssuclr-fas ,a.. burner ;3 7o whichcausesa blast of heated air and gases 4 through the cylinder 2., Crushedore maybe W fed to the hopper 1 incontinutaus manner by suitable means, and theidried product continuously discharged from the cylinderv mtoa. chute tavhich leads to 'a mill 510i suitable, construction, in which the-crushed ,ap jalication filed on jipril lst-f. 1910, Seia iNq.

552,846; entitled Metl'iod' and "apparatus for drying slimcs. The princ'ipleinvolyed" in mixture icontaming a sufficiently low .perccntagrc of nolsture to permlhthe maiss to-be" :disintegrateih is obtained, and, one ibe slimes are gendered better siiitcd for, cX- posure within the"d1fi 'e extractionof'inoist-urc. i A, a blower 0 may o rat'. 1mugapi i;e 7 1 to force air and theground mas's th'rpugh the mill and discharge chute S'i'nto'th'e ('OiYing end 9 of'the'ainphidizer 10, crime blower (i may operate throu'glrthe' 11," pipe 7 being closed, t0 force. air and the grouml mass, Iw hich -is fed by 'gtlif initl's through chute 8, through the feed end 49 of speciiical [y shown and" described "a prior application tiled"by' 'me on-ftuguslt' 31st, 1909, Self. No. 515,538. entitled Apparatus and method for au'iphi'dizing, an'd comprises a rotary-drum with a central'hezit-ingflue through which. lieatlinay be supplied;- if nccc. ary, by "a suitablejbin'ner'-l2 ",The] rotation of the drum operatestd'conduct the ore and 'air' through the drum inone direction and return, it in another tonthe only in starting operations, after which the U generation oflieat-liulheoxidation-of sulfur am] the" p I morciinsomeores the percentage of sulfur.

willnl'ai'iitaiir the temperature -Furtheris higher'ftlian that neededfor operating the linde'r 2 f r the -o5- i \I' vung, H

method, and ithat' by regulating the blower 6 the uantity of air supplied to fate and cppperjuilfate. If there is a dc 'ficiency offlsulfur in theore for maintaining oxidize the sul ur may be so adjusted as to limit the oxidation tothe desired amount, thereby controlling the temperature in-fthe.

i J hence of'air lift 30. The solution which amphidizer. I i.

As I have pointed out inc-myco-pending applicatiomfienilio. 515,538, the heat in the Q amplridizer'is maintained at a anama; mediate the dissociation points of ferric sulthe heat, I find that carbon may beadde for that purpose (in practice, ground upand mixed with the ore) without reducing, w the water soluble product of the amphidize'r,

'or, consequently, the extraction of values in the solution drum.

It is also tobenoted that with some ores the solutions employed in my. process seem to more readily take upthe values from sulfid remnants than from oxid remnants which again illustrates the necessity of 'maintaim mg a fixed temperature in the amphid'iz'er to prevent the production-offsuch oxid rem- The treatmentin the amphidizer- IQdevelrps considerable-dust and fumes, as al "descrihemand these may beled ofi "throughasuitable pipe 13- for abs'orptioninthe dust and jumes absorbing drum l4,' the traveloi' thefdu'st and fumes throu h thepipe la a'nd 14 being facilitated y the suction 1-5. The. absor tion of the will be descriiled detail;

' From-the amphidizer 10 a amps-mad substance, asses through'the chute. 16 into k in appear, withsolutionsfwhich dissolve but the neck 1 ofthe reactlon'dfum' 18 which is:

rotatable and suitably supplied, as will herethe values. Q Theparticular construction of thisidr um may be assumedf to be such that the oreis' agitated with the'soiution's a'ndthe mixture of solutions 'andsolids' discharged through' conduit 19, upon the filter bed 01'' beds 20. ,Ilhe filters may be assumed to be vacuum filters discharging through pipes: 21

and 22, the latter forming a columnfsutlt ciently hightoresist the vacuum which may be applied by pipe 23,- thepressure pipe 24 being closed. These pipes are respectively connected to suitable sources of vacuum and pressure, not shown, The filtered solution;

passes'from the pipe 22 into the well 25 and 'overfiows"throughoutlet 26; The depth of the'lwell-L2 5 is such that pressure applied through 'pipe'24=,"=vacuum pipe 23 being closed, may operate throu h pipe 21 and filter 'block 20 to blow ofi t cake when the filter is inverted. From the, outlet 26 the so: lutions pass into the oxidizer 27 wherein the salts of variable valency'are subjected to further treatment, (as by supplying air there- 1 later in 'cipitate may be se partially'or entirely diverted, when desired est 'deslred valencies, and the solutions are r then diyided, one portion (going through bypass 28, 29 to the dust an fumes absorbing drum 14, a ve'lreferredto, under the influpasses through the bypass, contains values {and salts combined at their. highestdesired 'valencies, andtheir eflect is thus, to oxidize and react with the dust andfumes'as indi- ,Similarreactions take place by the 'iron ,salts resent. a i

Re erring to the it will be seen that they pass through pipe 31 into a heater32 where their temperature is raised to facilitate precipitation. 'From the heater 32 they pass throughv pi precipitator 34 supplied throng hopper'35 with a suitable-precipitating agent such'as calcium carbonate or cupric oxid, whereby the iron and aluminum salts are precipitated from the solutions. ,The' precipitate is separated from the remainin solutions by a filter 36 operated as above escribed in connec- -'tion with the first filters, and the solution,

I division of the solutions which was not. directed through the b ass,

33 into a now containing among other substances copeater 37 to a precipitate! 38 w lch-is sup-J cupric hydrate, e co perhy r Elf and zinc salts, is led through ipe 37 and onate whereby-copper is precipitated as c '1} rate pixie rate from the remain-{i ing solutioniby fi ter 40 operated as above described 7 and] removed for "further treatment to obtain the metal, while thesolutioh,

which may still contain zinc values,- isleid through pipe41 and either returned. to the reaction drum 18 by pipe 42 or it ma through a bypass 43 and preclpltator Msup- I pl ed through hopper 45 with a suitable pre cipitatingagent such as calcium o'xid, where-5 by zinc is precipitated. The zinc recipitated may e separated from the solution filter46 operated as.abovedescribed andithe' solution returned' '"through -v pipe/17 to the reaction drum 18. 4

he use of calcium carbonate for 'pr'ecipi Ito tatin ,iton, aluminum and copper. co'm-- poun s fregenerates, calcium ch 1m for takin up as already indicated, 1 orid, whichi-is a solvent substance; 5 from which chlorid is supplied tofthe values-,1v It will thus be-seen that the-primary. solvent" or carrier solution is re enerated and delii' ered to the reaction further yalues. The-solutions containing.-

"parent.

man; od; :1."

the absorbed substances from the oust and fumes pass from the drum 14 through a jductindicated at 4L8, thence through a heating and agitating tank 49 whichmay have supplied thereto through pipe 50 an agitatmg 'gas or other substancesuch as a1I"0I" steam, which, may also have an oxidizing ettect f ClGSlI'Gd." From the heating an'd agitati ng tank'49 the solutions are then delivered through pipe 51' into the reaction drum 18. The absorption of the dust'and fumes in thenian'nerdescribed thus not only pre vents contaminationof the atmosphere by the'lfu mes, but at the same time makes use of themi' ""In' operation the system described makes it possible to recover the values from sulfur hearing. ores without any fumes being discharged into the atmosphere.

The reactions in thereaction drum and during the precipitation of iron, aluminum and copper, takeplacemore rapidly ifthe" solutions are heated to ahout'100 C. "The solution may'be'heated in the reaction drum or on it's way theretoas indicated diagrammatica'lly'bythc heating coilsz. The addition of oxygen to thesolutions, and the em-' ployment of 'vacuum filtration both cause reductions oftemperaturesx The purpose andfimportance of heating the solutions .at. 37 and will thus be .ap'.

the points In the ope ation ot-myprocess, the carrier solution is regenerated and used. .overand over again-in eycliomannerso' that there is g praetically noloss of solutions. Such heing the' c ,se, thenece. wit-y for economizing 1n the quantity of solutions maintained .1s j (lone away-Withfand therefore I prefer to maintam the s'oluti'i'ms in considerable excess. .Tn

this way the noces ityltor close observation hy'ithe attend-ant iselimin atecl, as, when I thecalciumchlorid is in excess-the operation can lie-carried on for .a consulerahle period of*ti me without depleting thesolutions of calcium chlorid even though the precipitator. may notice in operations: Tn other words,

an of calcium chloridgives an elasticity tothe system thus reducing the labor and in many cases theanalysis that. ,would otlierivise jbe necessary t o -maint ain a nice pounds involved.

Tn the 'specifi'c instance'of the carrying out :Of; my inven ti on described, herein, the

lmlanco-hotween the various chemical corn- 4 acid radical which intervenes in the solution to promote the shifting of the chlorin o t'the, calcium chloridii'ron'rthe calcium to the-values in the ore. is developed plainly in he amphidizcr in the form oi SO,,, but it not intended to limit-the invention to this the invention is gapable in this .pec'ts of: variations in many m oth'cif l.

. ways; i'vithi'n theylimitsof the appended It will be noted that in this system the solution of calcium chlorid acts both as a 1 solvent and as a. carrier, circulating through tlie'apparatus from the beginning to the end and when regenerated is restored to the beginning of the system ivithoutchange of :state; that the ehloridizing of practi ally the entire values takes place in the solution (lIlllTl and not in any preliminary roasting process; that there is'no tendency to overload the system with chlorln salts requiring expensive processes of elimination, and the,

the solution is kept automatically restored to proper condition with the calcium chlorid in excess of that normally required for taking up the values without additions, except those required to makeup for the slight waste that may occur.

What'I claim is:

1. The method of concentrating copper values, which consists in associating in a calcium chlo'rid solution the ore containin commingled values and gangue and an aci radical developed from the materials used in the operation, shifting the chlorin from the calcium chlorid to the values by the in tervention of the acid radical, so as to rep'lacc approximately all of the acid radical .=i n the ore by chlorin, precipitating the waste "products, separating the solutionv from the ates the carrier in condition-for re-use of substantially all of said carrier in the operation, and separating the precipitated values from the solution. V

- fThe method of concentrating copper values, which comprises converting substantially all .the copper content of a solution into copper chlorid, carrying the, copper chlorid: in a calcium chlorid solution, separatingthe solution from the gangue. and separating the values from the solution.-

;4. The method of concentrating copper values, which comprises dissol vi ng the val ucs from a commingled mass of values and gangue by a calcium chlorid solution, scparating the solution from the gangne, and reactlng upon the copper chlorid \Vll'll calcium carbonate to separate thc-valucs from the solution and regenerate the calcium chlorid.

5.'The method of concentrating copper values, which comprises converting the cop-1 per content into copper chlorid, dissolving the copper chlorid in a calcium chlorid solotion, separatingthe solution 'from the gangue, reacting upon' the copper chlorid with calcium carbonate whereby co per oxid is precipitated and calcium chlori regenerated, and separating the precipitate from the solution. v

6. The 'method of concentrating copper. values, consisting in producing in sg'tu an.

siderable excess ofthat normally requiredfor taking up the values. p v

8, The method of concentrating copper values which comprises treating thef sub-f stance bearing the values with a carrier solution containing dissolved solvent maintained in considerable excess'of," that normally requiredfor taking up the values, ie-

' moving values from the solution and reing the values with a carriersolution con-' turning the solution for the taking up of further values.

, 9. The method of concentrating values which comprises treating the substance beartaining dissolved solventmaintained in con: siderable excess of that normally required for taking up the values, separating. soluwhich regenerates the carrier solution.

values, which comprises treating a copper bearing substance with a carrier. solution containing calcium chlorid maintained in excess of that normally required'for taking up the values. p

11. .The method of concentrating'copper values, which comprises treating a copper bearing substance with .a carrier solution containing calcium chlorid maintained in excess of that normally required for taking a up the values, separating solutions from solids and precipitating the copper values from calcium chlorid is regenerated.

12. The method of concentrating copper values, which comprises amphidizing the ore, treating the commingled values and gunguc from the amphidizerwithcalcium the solutions by calcium carbonate, whereby f chlorid solution to dissolve the copper from the sulfate and produce cupric chlorid, dis

solving in such copper chlorid any copper" bearing remnants -chlorid and removing the copper from the insoluble in calcium solution. 13'. The continuous method of concentrat- 'ing copper values, which comprises treating values, which comprises dissolving -10. The method of concentrating copperf .thecopper bearing substance with a carrier which will dissolve the. values and preci itate the waste products, vfiltering'the so ution from the gen ue'and w'asteproducts, precipitating the va ues with a reagent which regenerates the carrier, separating the precipitated values from the solution and returnin the solution in acyclic manner substantia ly without change of state.

ing copper-values, which comprises treating the copper bearing substance with a carrier which will dissolve the values and precipitate the waste products, filtering-the solution from-the gan'gue,, and waste products,precipitatingthe values by a reagent which recopper ,per content into copper chlorid, dissolving the'copiper chlorid in a calcium chlorid so lution,

in a cycllc-manner. l

17.'The method of concentratin copper t e values in a calcium chlorid solution, solution from the gangue, separating the values from the solution, regenerating the the whole solution in a cyclic manner.

18. The method of concentrating copper values, which comprises converting the copthe ciiplper chlorid ina calcium chlorid solu tion, reacting upon the copper chlorid with ca'ljciiim-carbonate whereby copper oxid is'precipitated and calcium chlorid regenerated, separating the precipitatefrom the solution, and returning the solution in a cyclidmanner. 4 19. The method 'of concentrating copper values, which comprises treating the copper bearing substance with a carrier which will dissolve the values and precipitate the waste prodi1cts, filtering the solution from the gangue, and waste products, precipitating values from the solution, and returning substantially the whole solution in a cyclic mare generates the carrier, s'e aratingthe pr'eci pi-- calcium chlorid, and returning substantially per. content into copper chlorid, dissolving.

11-0 teringthe solution from the gangue;

14;. The continuous method of concentratwhole solutionin a cyclic values, which comprises convertingthe cop- I ltering the solutionfrom the gangu'e separating the'valu'esTrom the'solution, an returning. substantially the whole solution tions from solids and precipitating the" values from the solutionsby a substance tering the the values from the. solution, filtering. the

I 20. The method of'c'oncentrating copperyalue s, which comprises treating the copper bearing substance with a carrier which will. dissolve the'values andprecipitate the waste products, filtering the solution from the gangue and waste products, precipitating the values a reagent whichregenerates'the earrier,. tering the precipitated values from the solution, and returning substantially the whole solutioninacyclicmanner; I Y 1 '21. 'Ihe'method of concentrating copper I 1 values, which comprises dissolving the-values in a calcium chlorid solution 'filtering the j soIution from the gangue, precipitating'thefvalues'from the solution, filtering the values 51 from th solution, and returni substam f tiallythewhole solution in acyclic manner.

'22. The method of concentrating copper.

values, which'comprises converting the copper content into'c'opperchlorid, carrying the I go copper .chlorid in a'calcium chlorid solu,-

from-"the solution, regenerating the'calcium chlorid, and returning substantially the whole solution in a cyclic manner. I

24. The method of concentrating copper values, which comprises converting the copper content into copper chlorid, carryingthe copper chlorid ina calcium chlorid solution,

filtering the solution'from the angue, reactingupon thejcopper chlorid with calcium 140' carbonate-whereby copper oxid is precipi- --tated and calcium chlorid regenerated, filtering"the precipitate from .the solution, and returning ubstantially the whole solution in we cyclic manners I '25L The continuous method ofconcentrab rig-values, which. comprises continuously circulat ng. a solvent an carrier solution in cycliemanner throu h the steps of dissolv- "ing; values,;with. ormat-ion of insoluble c'ts. on -solutionsgseparating values ro m solutions, and r'egenerating solvent material. 26., The continuous method of concentrat-i I ngvalues, which comprises continuously cir- 5 culating' a. solvent and carrier solution in lic manner through the steps of dissolv- .values with. formation of insoluble waste oducts, .filtering' solutions from said waste ions and: regenerating solvent. material, and fil e n pi ed va ueein sel @Thecontinuous method of concentrating "values, which comprisescoritinuoudfi amphid zingath ie ppse be ing s nc t as wastegroducts, eliminating said waste. ro-

I from the solution. pnoducts,..x precipitating values, solucarrier solution in cyclic manner through .the steps of dissolving values from the amphidlzed substance, eliminating gangue from solutions, separating values from solutions, and regenerating solvent material.

28. The continuous method ,of concentratingvalues, which comprises continuously amphidizing the copperbearing substance, i

and continuously circulating a solvent and carrier solution in cyclicmanner'through the steps amphidlzed substance, filtering solutions from gangue,.precipit'ating values from solw tions and regenerating so vent material, and 'filterin precipitated valuealfrom solutions.

29. he method of concentrating copper values which comprises causing the circulaof dissolving valuesfrom the l ,tion' of a-carrier solution containing chloridin excess of thatxnormally-re uired for tak-' ingup thevalues inth'e ore to e treated, the

ore being first treated with said solution to dissolve the values and precipitate the waste products, the solution thenseparated from the gen e and waste products carrying:

. with it t 0 values, thev'alues then separated from the solution and the solution restored to'its normal condition with the chlorin carrier'in excess, and returned for the treatment of further copper bearing substances.

. 30. The method of concentrating copper values, which comprises. continuously treating the-copper bearing substance with a carsolution from the gangue, separating the air rier solution containin dissolved solvent for values from the solution and returning substantially the whole ner.

32. The method of concentrating copper values, which comprises continuously amphidizingthe copper bearing substance, to produce in combination with substantially all the values an acid radical which is interchangeable in calcium chlorid solutions, continuously carrying the values in calcium chlorid solution, se arating the solution from the gangue, an separating the values solution in a cyclicman- 33, The cyclic process'of concentrating metallic-values from ores which consists in amphldizlng such values to produce incom- I eium'chlorid' solutions, continuously adding and continuously circulating a solvent. and

the resultant to a solution of calcium chlorid, continuously agitating said solution and mass, separating the ga'ngue 'from'the solutionand 'precipitati-ngthe values from the solution.

I "34-; The cyclic. process 'of 'concentrating metallic values from ores, which consists 1n amphidiamg. such values to produce in combination with substantially all the values an acid radical which is lnterch-angeable in calcium chlorid solutions, continuously add ing the resulta ntjmassto a solutionof calcium chlorid, continuously agitating said solut on and mass, separating tliegangue from the solution, precipitating the values "from the solution, and return'ingth'e'solution for continuous addition of preparedore.

35..T-he continuous method of c'once'ntrat' ting values, which comprises" continuously :circulating a solvent and" carrier solution "containing an acidlexchangingi salt and a salt of an element of variable valency in cyclic manner through the steps ofdissolving values with formation ofinsoluble waste products, eliminating said waste roductjs rom solutions, separatingvalues rom solutions and regenerating solvent material.

,36. The continuous methodof concentrating values, which comprises continuously circulating a solvent and carrierisolution containing an acid exchanging salt and a salt of an elementofvarlable valency in' cyclic manner through the steps of dissolv- I ing values with formation of insoluble waste products, filtering solutions from said waste products, precipitating values from solu tions and regenerating solvent material, and

filtering precipitated values from said solu'-' tions. I r v 37. The method of concentrating copper values, which comprises treating the copper bearing substance with 'a carrier solution ,containing an acid exchangingjsalt and a salt of an elementof variable valency, precipitating the copper with .a substance to restore the acid exchanging salt while retaiuing a portion of a salt of an element of variable valency, and returning, the carrier solution to, the further treatment of copper values.

38. The continuous method of concentrat ing values, which comprises continuously v circulatingv a ,solvent I and carrier solution containing acid-exchanging salts and. a salt" ot an. element of'variable valency in cyclic values with formation 9 products, ehmmatmg' said .waste products om solutions, separating values from solu:

mg values, which comprises continuously.

manner through the ste s of dissolving insoluble Waste tions and regenerating solvent material.

39. The continuous method of concentratcirculating a solvent and carrier solution containing acid exchanging salts and a salt "of an element of variable valency in cyclic manner through the steps of dissolving turning eratlons.

values with formation of insoluble waste p'roducts,filtering solutions from saidwaste products, precipitating values from solutionshnd regenerating solvent material, and

filtering precipitated values from said solutions. r

40.The method of concentrating copper values, which comprises treating the copper bearing substance with a carrier solut 1on.

containing an acid exchanging salt andsalts of elements of variable valency, precipitating the copper'with a substance to restore the acid exchanging salt while retaining a portion of'the salts of elements of va-ria'ble valency, and returningthe carrier solution to the further treatment of copper values;

llAThe m'ethodo'f concentrating copper values, which comprises treating the copper bearing=substance with a carrier solution containing an acid exchanging salt; and-salts of elements of variable valency, precipitating the copper with a substance to restore the acid exchangin salt While retaining a portion of a salt 0' an element of variable valency,'and'returning the'c'arrier solution a to'jthe further treatment ofcopper' values.

"42. The methodof concentrating values,

which comprises taking into solution salts of variable valency, continuously maintaining the'salts at their highest valency,- an'd precipitating values from the solutions containing the'salts at their highest valency.

l3llhe method of concentrating values from'salts of elements of variable valency,- Which consists in taking the values into solution, dividing the solution, precipitating the values from one division while maintaining the salts at highest valency-and reboth divisions to the cycle of 0p- 44. The method of.concentrating values, which comprisestaking into solution salts of variable valency, maintaining the salts at their highest yalency, dividing the solu-' tions, precipitating values from one division while its salts are at'highest valency, and -rettn-n'ing the other division still con:

,taining the salts at'their highest valency to the dissolving of further values.

45.*The method of concentrating values,

which comprises takin into solution salts of, variable valency, maintaining the salts at their highest valency, precipitating values regenerating solvent material, and returnp solution, absorbing the dust and fumesjm one division'while the salts are at highest valency, and precipitating values from the otherdlvision while the salts are at highest valency. 1

48.- The method of concentrating' values,

which comprises amphidizing the'substa'nce containing the values, collecting the ,dust and fumes therefrom, takin into solution as salts of 'variablevalency .t e values from the amphidized substance, maintaining the salts at their highest valency, dividingthe solution, absorbing the. dust and fumesiu one division. while. the'salts are athighest I valency, precipitating'valuesand regenerating solvent-"material in the other division while the salts are at highest valency, and

j returning thev divisionwithabsorbed dust and fumes and the divisionwithregenerated solvent'material to the dissolving of further values.

' ing substances, which comprises oxidizing the active portions of the substance, collooting the volatile products of oxidation in a carrier comprising, a salt capable of exchanging acids in combinationw1th salts of variable valency, subjecting the substance to suchcarrierwhereby the values are takeninto solution, separating the solution 40 from the gan ue, andpprecipitatingthe.

values by asu stance which restoressaid acid exchanging salt.'- I v j 501 The method oftreat'ing copper bear- .ing substances, which comprises oxidizing 5 the active portions of the substance,collecting the volatileproducts of-oxidation iii a calcium chlorid' carrying and transforming solution, subjecting the substances-to suc carrier whereby t e gangue,, and precipitating. the .values by a substance which restores calcium chlorid to l; the solution.

-51.. The method off concentrating values, I which-comprises amphidizing the substance,

bearing. the, values, collecting. the'dust and fumes therefrom, dissolving values from the iamphidiz'ed substance in a primary solvent, dissolving in the dissolved valuesportions c0 of values insoluble'in the primary solvent, andabsorbing the; dust andfumes in, s0lu tions'thus formed.

- .52; The method of concentrating v'alues,

' which comprises amphidizing the substance 7 05 hearing the values, collecting the and solvent, 1 49. The method of treating copper bear- I n values are taken into sosolution, separating the selutionfrom'the fumes therefrom, dissolving values from the amphidized substance in a primary solvent whereby such values are converted into a secondary solvent, dissolving in the secondfar solvent values insoluble in the primary so vent, and absorbing the -dust and fumes in solutions thus formed. v 53. The method of concentrating values, which comprises amphidizing the substance bearing the .values,collecting the dust and fumes therefrom, dissolving values from the a'mphidized substance in a primary solvent, dissolving in the dissolved values portions of values insoluble in the primary solvent, separating solutions from the angue, di- 8 viding the solutions, absorbing t e dust and fumes in one division, recipitating and separating 'values from t e other division and regenerating the primary solvent therein, an returning the two divisionsthrough 5 the cycle of operations. 54. The method of concentrating values,

whicheomprises amphidizing the substance bearingtliewalues, collecting the dust and fumes therefrom, dissolving values from the amphidized substance in a primary solvent whereby such values are converted into a secondary solvent, dissolving in the secondary solvent values insoluble in the primary separating solutions from the gangue, dividing the solutions, absorbing the dust and fumes in one division, precipitating and separating values from the other division and regenerating the primary solvent therein, and returning the two di- 10 visions through the cycle of operations.

55. The method of concentrating values, which comprises amphidizing the substance bearing the values, collecting the dust and fumes therefrom, dissolving values from the 1 05 amphidized substance in a primary solvent,

dissolving' in the dissolved values portions of values insoluble in the primary solvent, separating solutions from the gangue,- dividw" 'ing the solutions, absorbing the dust and fumes in one division, treating the othenrlivision with a substance which precipitates values and regenerates the primary solvent, separating the precipitate, 1 and returningthetwo divisions of solution through the cycle of operations.

56.;The method ofconcentrating values,

- which comprises amphidizing the substance bearing the values; collecting the dust and fumes therefrom, dissolving values from the amphidized" substance {in a primary solvent whereby such values are converted .into a [secondary solvent, dissolvin'gin the secondary solvent values insoluble; in the primary "solvent, 'separating-" solutions from the 'gan'gu'e, dividingythe solutions, absorbing the dust andfumes in'one division, treating jthe'other division witha substance-whi h precipitates values and' 'regenerates the primary' solvent therein, separatingthe precipitate, and-returning the two divisions of so- 57.-- The method ofconcentrating values of copper bearing substances, which comvpr sesthe' treatment of suchsubs'tances in an an phidizer and bringing (the dust and fumes therefrom in contact with a calcium chlorid solution.- l l 58; The method of concentrating values which jcom risesamphidizingjthe ore,i taking the va ues into solution,collecting-the dust from amphidizing in the solutions and transferring the solutions with the dust.

i6 The method of-concentrating vfnii's the dissolving of-further values.

whichgcom rises amphidiaing the ore, :tak-. ing the va ues into solution; colleeting qth'e dust and fumes from, the" amphidizin'g, in

adding oxygen' tojthe solutions,- and transa ferring the solutions containing dust and oxygen to the dissolving of further values."- 561..The mthod'of concentrating values so ,the solutions and transierring the solutions,

to ;the-.dis'-;

containing the dust and fumes solvin of furthervalues; Q

'60. he method oi concentrating. values, which com rises amphidizingthe ore, tak ing the-va' use into solution, collectingsthe dustfrom 'amphidizing' inthe solutions,

which comprises amphidizing the ore, takingj the values into, solution, collecting the I dust and fumes from anphidizing in the solutions, adding oxygemtothe solutions, and transferring the solutions ieontainingdust, fumes and oxygen the-dissolving ot'ffur- (62L The method of ltoncentrating values, which icor'nprises amphidizing the ore, tak-.

ing the values into solution as ic chlorids, collecting the. volatilejfproducts" from amphidizing 'in 1- the ji'solutions, adding 1 oxygen .to the solutions, and transferring the solutions ,to thedissolvingof further values, 1

' Q63."'Thef methodfof concentrating values,

which comprises amphidizin'g theb're, taking the values into solutionas' in chloride and dissolving them in calcium ehlorid'solution, collecting the volatileproducts from amphid'iz'ing in'the solutions, adding-oxygen to the solutions, and transferring the soluti'ons to the dissolving offu'rther values;

64. The niethod of concentratingvalues, which comprises amph'idizi'ng the ore, taking the-values into solution, collectingithe volatile amphidizer products? inQtheP'dissolved values,- adding" oxygen to'f the solutions, heating the solutions, and transferring the heatedsolution sto the dissolving; of further values. v 65. The method of concentrating values,

.comprisingoxidizing the substance hearing such values, dissolving the volatile products .of the oxidation 3 at low .temperaturq heat- ,i-ng the solution ,and using it to dissolve'the v 5 oxidized substance at higher temperature.

lution through thecycle of operations.-

66.'The method of concentratlng values,

and .vvashing the soluti'on from the gangue, bringing the volatile products of oxidation into contact'with the'solution and partially evaporating the added washing water.

cues in copper bearing substances, comprising amphi'dizing such substances, treating the non-volatile part of such substances in a tion,'. comrningling the two 'solutions, prorating the solutionl froni the gang'ue and 'separating-.the values from the solution.

, 68. Themethod of concentrating the val- -ues in, copper bearing substances, comprising non-volatile part "of such substances in a "calcium chlorid' solution, treating the volathe two solutions, producing and vdissolving copper jchlorid, separating the solution from the gangu'c and separating the values from the solution; I

the non-volatile L a calcium chlori solution, treating the 'vol. "atile'partthe 'iin' a scparate body of soluthe solution, dividin'gflthe solution, precipidivision of the solutl'om? divis'lons-ofthe solution to "-the 'cycle of operations;

values, which comprises dissolving values 1n solved: is hespprtions of values insoluble in from the; gangue, dividing the solutions,

one division an primary"-solven andy retnrning the two divisionstlirough the cvclii df operations- 73. 'lfhc cxclic method of concentrating calcium chlorid solution, treating the v ol'a tile partthereofin a separate body of soluducing and dissolving copper chlorid, sepaamphid-izing such substances, treating the r,

-" '69.,The method of concentrating the val; I "ues' in 1 copper bearin substances, compris ingamphidizing suc 'substances,.treat1ng rt of such substances in tion, meeting; the soluti'on, commingling the a :per vchloridfse arating-the solution from.

consists in takingthe values {Into solution, eliminating the gangue' from I tatingand removin "tli ,values 'fronr-onef d'returningboth 72'. The cyclic oi 'concentrating apprifna '-solvent, dissolving in the dis- 1 precipitating and separating values from d *regenerating' therein thecomprising oxidizing the substance con'tainingjvalues, dissolving the values, filtering 67 ."The method of concentrating the valtile part thereof in a separate body of solu- I 'tion, oxidizing the solution, ,c'ommingling ice the primary-solvent, s eparatin'gf solutions.

7' time from the as I calciumchlorid' in excess efthat normallythe solution from the I f tating' and filttr ing the values from the soa5, lution.

a. primal} solvent, whereby such values are "converte into a secondary solvent, dissolving in such'secondary solvent values insolublexin the primary solvent, se arating solugangue, divi ing the solutions, precipitating and separating values from-one division and regenerating therein the primary solvent and returning the two divisions throu h the cycle of operations. 74. Th'e c"cl1c methodjof concentrating 5. values, whic comprises dissolving values in av primary solvent, dissolving in the dissolved values portions of values insoluble in the primary solvent, separating solutions from the gangue, divid ng the solutions, treating one division with a substance which precipitates values and regenerates the primary solvent, separating the precipitate, I and returning the two divisions t rough the cycle of operations: I 75. Thecyclicmethod of concentrating values, which comprisesdissolving values in a prima solvent whereby such values are converte into a secondary solvent, dissolvingin the secondary solvent values insolu- -ble in-the primary solvent, se arating solutions .from thergangue, divi ing the solutions, treating one division with a substance which precipitates values'andregenerates '7 the 'primarysolvent, separating the precipitate, and returning the .two' dlvisions through the cycle. of operations.

76. The method ,of concentrating copper values, which comprises dissolving the values ina calcium'chlorid solution containing required for-takin up the values filtering the solution from t a waste products androcovering the values.

77. The method -of"'concen tratlng copper values, which comprises dissolving the'val-v ues in -a'calcium chlorid solution containing calcium chlorid in excess of that normally required tor takin up the values, separating the solution cm the waste products, precipitatingthe values and filtering the values-from the solution.

78. The methodof concentrating copper f values, which comprises dissolving the. values' n a calcium chlo'rid solution containing calc mchlorid in excess of-that normally required for taking up the values filtering gangue, and p'recipn 79. The method of concentrating copper .yalues, which comprises convertingthe copper content-into copper chlorid, carrying the copper chlorid in a calcium chlorid soof that required for taking up the values, filtering the solution from the gangue, and precipitating and filteringthe valuesfrom 1 the solution.

80. The method 'of concentrating copper acting upon the copper chlori into solution, precipitating r nd 'that required for takingtupthe values,'filtering the solution from the angue, re- -gu w1t h calcium carbonate where copper oxid is precipitated and calcium chlond regenerated.

.and' filteringthe precipitate from the solution. r "at 82. The cyclic method of concentrating values, whic comprises taking the values theiva'lues regenerating solvent-material :in the .tion, separating the precipitate from thesoo lution by vacuum filtration, and heating and returning the re nerated solution to the dissolving-of furt or values.

83. The method of concentrating jvalues in substances containingcopper in associags: tion with other-metals, comprisingtakinizthe metals into solution by the employmen of'anacid exchanging salt, separating the gangue from the solution, precipitatinghthe' values from the solution by a reagent 'w ich 10o regenerates the acid exchanging salt in condition for reuse. in the operation without chenge'of state, separating the values from the solution, and returning the solution to the cycle of operations. 1.105

84. The. method of concentrating values from co perbearingsubstances, whlch com prises issolving iron and copper com-' in a primary solvent whereby such compounds are converted-into solvents for values insoluble in the primary solvent,

se arating solutions from the gangue" d1-' viding the'solutions, precipitating the vdlues iromone division while retaining the values in solution in the other division, and return- 116 in the solutions still contaimn the dieso ved values to the treatment" 0 the. copper bearing substance.

85. The method 'of concentrating from copper bearing substances, which com- 1 20 prises dissolving iron and copier compounds y suc m a primary solvent where comunds are converted into solvents for values ;1nso1uble in the qrimarv solvent, separating lution containing calcium chlorid in excess 0 solutionsfrom s ds, dividing the solutions precipitating values from one division and regenerating therein the primar solvent, while retaining the values in so in the other division, and returning: bfeollitim still containing the dissolved values 'aadthe lab bearing substance.

solutions containing the regenerated 'pri mary solvent to the treatment of the copper 86. The method of'obtaining substances from their solutions, comprising treating a. solution containin and zinc oompoun s with calcium carbonate whereby i' on, aluminum and copper values are precipitated solu'tionwith calcium oxid whereby zinc valles are precipitated.

,' iron, alum 1num, copper. 1

and treating the remaining The method of concentrating rallies; J

which comprises treating acopper bearing substance containing arsenic w1thcalcium ChlOXId solution, whereby coppercompounds 15 "are dissolved and the arseniocontent rendered insoluble and precipitated, separating solids from solutions; and recovering the values 'from the solutions CHARLES s; BRADLEY. Witnesses: Y H. 'H. KNIGHT,

' CLARA HOHENS'ITEIN. 1 

